首页> 外国专利> Process for the production of the spiroglycol 3,9-bis(1,1-dimethyl-2-hydroxyethyl)-2,4,8,10-tetraoxaspiro5.5undecane

Process for the production of the spiroglycol 3,9-bis(1,1-dimethyl-2-hydroxyethyl)-2,4,8,10-tetraoxaspiro5.5undecane

机译:螺二醇3,9-双(1,1-二甲基-2-羟乙基)-2,4,8,10-四氧杂螺[5.5]十一烷的生产方法

摘要

In the production of spiroglycol by the reaction of pentaerythritol and hydroxypivalaldehyde in water in the presence of an acid catalyst, (A) a total content of amines and amine salts in hydroxypivalaldehyde is reduced to 1.5% by weight or lower; (B) seed crystals are added to the reaction system before initiating the reaction and/or during the reaction in an amount from 1.5 to 30% by weight on the basis of the total feed amount of pentaerythritol, hydroxypivalaldehyde, water, the acid catalyst and the seed crystals, each being fed into the reaction system; (C) the pH of the reaction system is kept from 0.1 to 4.0 from initiation of the reaction to completion of the reaction; and (D) the sum of a maximum theoretical amount of spiroglycol to be synthesized from pentaerythritol and hydroxypivalaldehyde to be fed into the reaction system and an amount of spiroglycol contained in the seed crystals to be added to the reaction system is controlled within a range from 5 to 35% by weight on the basis of the total feed amount. The spiroglycol produced has an increased particle size. By washing the spiroglycol with a basic solution, the heat stability is improved.
机译:在季戊四醇和羟基新戊醛在酸催化剂的存在下通过在水中反应生成螺二醇时,(A)羟基新戊醛中胺和胺盐的总含量降低到1.5重量%或更低; (B)在开始反应之前和/或在反应过程中,以季戊四醇,羟基新戊醛,水,酸催化剂和籽晶,分别注入反应体系中; (C)从反应开始到反应结束,反应体系的pH保持在0.1〜4.0。 (D)将由季戊四醇和羟基新戊醛合成的拟合成的螺二醇的最大理论量加到反应体系中,将加入到反应体系中的晶种中所含的螺二醇的量控制在以下范围内:以总进料量为基准,为5-35重量%。所产生的螺二醇具有增加的粒度。通过用碱性溶液洗涤螺螺二醇,提高了热稳定性。

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